Method for Manufacturing a Hydrogen-Added Water and a Device for the Same

ABSTRACT

The object of the present invention is to provide a method for manufacturing the hydrogen-added water containing a large amount of the microscopic bubbles and a manufacturing equipment for the same so as to expand the industrial applicability of the hydrogen-added water by containing the large amount of the microscopic bubbles. More specifically, a plurality of tubular structures, in which the diffusion chamber  5  having the double tubes is provided, and the porous element  6  having predetermined pore diameters in the diffusion chamber  5  are provided, are substantially linearly arranged in a longitudinal direction. The raw water and the hydrogen are supplied with one of the tubular structures, so as to form the mixture fluid of the raw water and the hydrogen by mixing the supplied raw water and hydrogen in the diffusion chamber  5 . The mixture fluid is passed through the porous element  6  and diffused therein. The mixture fluid of the raw water and hydrogen passed through the porous elements  6  is supplied with the adjacent tubular structure under high pressure so as to mix it with the hydrogen in the diffusion chamber  5  of the adjacent tubular structure as well as to pass it through the porous element  6  and diffuse therein. Consequently, the hydrogen-added water containing a large amount of the microscopic bubbles of the hydrogen gas can be continuously produced.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to a method for manufacturing a hydrogen-added water and a device for the same, more specifically, relates to the method for continuously manufacturing the hydrogen-added water containing a large amount of microscopic bubbles of the hydrogen gas and the device for the same.

2. Related Art

Various oxidation-reduction systems are present inside of the body of mammals including a human (hereinafter, referred to as “living organism”), many of which conjugate to one another and are involved in the oxidation-reduction reaction inside the living organism. An oxidation-reduction electric potential in the oxidation-reduction systems inside the living organism is directly concerned in the free energy changes of the reactions and equilibrium constants, thereby help predicting the direction of the reactions.

The oxidation-reduction reactions of mammal organs or the reaction inside the living organism have low electric potentials that are normally in the range of −100 mV to −400 mV, the pH of which is in the range of 3 to 7. It is understood that as the oxidation-reduction potential in body fluids is increasing, an active oxygen is easy to be remained, thereby causing organ failures. Especially, in the intestine that enteric microbes are very active and that digests and absorbs nutrient components, anaerobic reducing ambient needs to be maintained.

For example, the oxidation-reduction potential of “acetic acid+CO₂+2H⁺/α-ketoglutarate reaction” within the living organism is −673 mV and the oxidation-reduction potential of “acetic acid+CO₂/pyruvic acid reaction” is −699 mV. The oxidation-reduction potential of “acetic acid+2H⁺/acetaldehyde reaction” is −581 mV and the oxidation-reduction potential of ferredoxin is −413 mV. The oxidation-reduction potential of “xanthine+H⁺/hypoxanthine+H₂O” is −371 mV, the oxidation-reduction potential of “uric acid+H⁺/xanthine+H₂O” is −360 mV. The oxidation-reduction potential of acetoacetic acid+2H⁺/β-hydroxybutyric acid reaction” is −346 mV and the oxidation-reduction potential of “cystine+2H⁺/2 cysteine reaction” is −340 mV.

Thus, in the reactions of enzymes, coenzyme and metabolically-related substances within the living organism, the oxidation-reduction potential is in the low environment. Also, a water or food product having low oxidation-reduction potential have separating and eliminating effects of the active oxygen oxidizing the body and molecules or atoms containing one and more than unpaired electron, i.e. free radicals, thereby enhancing the reaction of the active oxygen excisionase called SOD (superoxide dismutase).

A body fluid provides grounds for metabolic reactions inside the body, including the oxidation-reduction reaction. The body fluid accounts for substantially 60% of the living organism, to which electrolytes, proteins, with a central focus on the water or the like are significant components. This is because the water, which the oxidation-reduction potential is low, is effective for within the living organism.

Meanwhile, the oxidation-reduction potential of a tap water is +400 to +800 mV, the pH of which is in the range of 6.5 to 8. Consequently, it is believed that the tap water does not keep balance with the living organ of which the oxidation-reduction potential is in the range of −100 mV to −400 mV.

Currently, as a method for lowering less than zero the oxidation-reduction potential of the water (for example, the tap water) that is in a mixed state of oxidant and reductant, an electrolysis method and a high frequency current impressed method or the like are proposed, However, in all methods thereof, the balance between the oxidation-reduction potential value and the pH is not ideal in terms of the oxidation-reduction reaction within the living organism.

Among the biological reactions, many reactions accompany the oxidation-reduction reactions and play pivotal roles in the metabolic reactions or the like. Also, beyond the living organism, in the system (solution) containing the oxidant and reductant, if the inactive electrode that is uninvolved in the oxidation-reduction reactions of itself such as platinum is soaked into the solution, a potential difference appears between the electrodes. The potential difference is the oxidation-reduction potential (Oxidation-Reduction Potential=ORP), the unit of which is referred to as mV. Herein, if an activity of the oxidant of a substance is [Ox] and that of the reductant thereof is [Red], the state that both are mixed is represented by the formula (1).

[Ox]+ne→[Red]  (1);

wherein e is an electron, and n is an electron number that is moving.

The oxidation-reduction potential (EmV) of the electrode reaction formula represented by the formula (1) is expressed by means of the Nernst's formula (2).

E=E ₀+(RT/nF)ln [Ox]/[Red]  (2);

wherein R is a gas constant (8.31 Jmol⁻¹K⁻¹), T is an absolute temperature (K), and F is a Faraday constant (96406 JV⁻¹). E₀ is a standard oxidation-reduction potential when [Ox] is equal to [Red].

In the formula (2), ln [Ox]/[Red] is a natural logarithm. Accordingly, as the denominator “[Red]” is extremely larger than the numerator “[Ox]”, the minus value of the oxidation-reduction potential E is increased. In other words, theoretically, as the activity of the reductant [Red] is larger than that of the oxidant [Ox], the oxidation-reduction potential can be negatively charged.

More specifically, in the method of making the oxidation-reduction potential of a raw water charge negatively by blowing the hydrogen into the raw water that is in a mixed state of oxidant and reductant, it is important that the activity of the reductant [Red] is larger than that of the oxidant. In this case, it is preferable that the efficiency is increased by blowing the hydrogen into the raw water, which is in the mixed state of oxidant and reductant, contacting it with reduction catalyst that metal is supported with the quartz porphyry.

The inventors have hitherto developed some hydrogen solution manufacturing equipments based on the above-mentioned theoretical background (see JP 2005-177724). In particular, JP 2005-177724 discloses a hydrogen-added water manufacturing equipment, comprising a reaction tank, a raw water-supplying pipe watertightly connected to the reaction tank, a depressurizing pipe watertightly connected to the reaction tank, a hydrogen-supplying pipe watertightly connected to the reaction tank, a product water-extracting pipe watertightly connected to the reaction tank.

At the same time, recently, studies for the microscopic bubbles and developments in application thereof have been well-practiced. The microscopic bubbles are defined as fine bubbles having diameters in the range of 10 to a few dozen μm. In general, the bubbles generated or formed in water have a few millimeters in diameter, but the microscopic bubbles are characterized by having hundredth thereof in diameter. In such characteristics, the microscopic bubbles have the high absorption efficiencies into the body fluids, and are superior in homogeneity and dispersibility. The microscopic bubbles also increase biological activities of the living organism. The applications to diagnosis and therapy of cancer are developed by taking advantage of the characteristic that the microscopic bubbles can produce heat up to about 70 degrees when they are exposed to ultrasound waves.

SUMMARY OF THE INVENTION

The present invention relates to a method for manufacturing a hydrogen-added water and a device for the same so as to solve the above-mentioned conventional problems. An object of the present invention is to provide the method for manufacturing the hydrogen-added water containing a large amount of microscopic bubbles and the device for the same, by adding the hydrogen-added water disclosed in JP 2005-177724 to a large amount of microscopic bubbles so as to improving the industrial applications of the hydrogen-added water.

The hydrogen-added water of the present invention contains a large amount of hydrogen, the oxidation-reduction potential of which is kept below −400 mV and the pH of which is kept slightly higher than 7. The hydrogen-added water contains a large amount of the hydrogen gas as the microscopic bubbles having the diameter in the broad range of milli-bubble, micro-bubble and micronano-bubble.

Herein, according to the microscopic bubbles, the diameters of the bubbles during the development period are sometimes classified into the milli-bubble, the micro-bubble, the micronano-bubble and the nano-bubble. The diameter in the millimeter scale is classified into the milli-bubble. The diameter in the range of 10 to few dozens micrometer is classified into the micro-bubble, that in the range of several hundreds nanometers to 10 micrometers is classified into micronano-bubble and that in the range of less than several hundreds nanometers is classified into nano-bubble. In the present invention, the classification is adopted. More specifically, in the development period, the hydrogen-added water of the present invention is characterized by containing the bubbles of the hydrogen gas having the diameters in the broad range from the milli-bubble that is below 0.12 mm in diameter to the micro-bubble and the micronano-bubble.

The inventors studied the following problems: (1) assuredly blowing a predetermined amount of the hydrogen gas into the raw water, (2) making the hydrogen gas contained in the raw water the microscopic bubbles having a prescribed diameters, (3) not batch-wisely but continuously manufacturing the hydrogen-added water and (4) requiring no broad installation space, occasionally having mobility like showers and being easy to operate.

Consequently, first, the manufacturing equipment according to the present invention has a tubular structure, a cross section of which is mainly circularly or rectangular formed. The material of the tubular structure is preferably metal as a carbon steel, a stainless steel or the like, but it may be a glass, a plastic, a ceramics, a rubber or combinations thereof having the strength enduring the negative pressure.

An aperture is formed as an injection tip of the water on one end of the equipment, to which the raw water-supplying system that supplies the raw water under high pressure is watertightly connected. The raw water-supplying system is connected to the water-supplying equipment of which a water pressure is 0.1 to 0.5 MPa, usually to the tap water, and a pump is connected in between. The supply of the raw water is preferably 8 to 20 L/min.

A nozzle is formed on the inner side of the tubular structure in the injection tip of the water provided on the other end of the equipment so as to inject the water injected under high pressure, under further higher pressure. As the raw water is usually injected in an incompressibility condition, i.e. below at sonic speed, the configuration of the nozzle may be so-called tapered nozzle so that a flow passage area is smoothly appropriately small. Preferably, when the raw water is injected in a compressibility condition, i.e. above at sonic speed, the flow passage area must be broadened again, so that the nozzle combined the tapered and divergent nozzles is used.

The hydrogen-supplying system is watertightly provided in the equipment. The system supplies the hydrogen substantially at a right angle toward the raw water supplied from the raw water-supplying system. Probably, a check valve is provided in the hydrogen-supplying system, thereby preventing the water supplied from the raw water-supplying system from flowing backward to the hydrogen-supplying system. A hydrogen cylinder, a gas pressure controlling device and a piping or the like are incorporated in the hydrogen-supplying system, thereby injecting the hydrogen gas to which the pressure is adjusted.

Preferably, the supply pressure of the hydrogen gas is preferably 0.2 to 08 MPa and the supply thereof is 0.1˜1 L/min.

In the tubular structure, a diffusion chamber is formed as so called double tubes in a longitudinal direction of the equipment, in the downstream of the hydrogen-supplying system, said diffusion chamber spreading a mixed fluid of the raw water supplied from the raw water-supplying system to the tubular structure with the hydrogen supplied from the hydrogen-supplying system to the tubular structure.

The diffusion chamber is formed so as to taper from both ends toward the center, i.e. to narrow down, so that the negative pressure is generated at the narrowed portion. Thus, a suction effect of the mixed fluid of the raw water supplied from the raw water-supplying system to the tubular structure with the hydrogen supplied from the hydrogen-supplying system to the tubular structure is increased, because the diffusion chamber is formed so as to narrow down, so that the negative pressure is generated.

Porous element having predetermined pore diameters is filled with the diffusion chamber. The Porous element provided with the diffusion chamber is a filter of a sort. Bubbles having the same diameters as the pores formed in the porous element can be produced by injecting the mixture fluid consisting of the raw water and hydrogen introduced into the diffusion chamber through the porous element.

The porous element has the pores having the diameters in the range of 120 μm to 2 μm, the material of which is not particularly limited and, for example, sintered body such as a gunmetal, a bronze, a nickel, a stainless steel, ceramics, and a metallic mesh or the like are available. The sintered body such as the stainless steel is preferable due to the abrasion-resistance when the produced hydrogen-added water is supplied for drinking.

The shape of the porous element includes a wide variety of shape such as a disk-shaped, a cylindrical shape, with a cylindrical bottom, with a base or the like. The cylindrical shape is preferable to insert it into the equipment.

The thickness of the porous element is 5 to 20 mm, preferably 5 to 10 mm, but is occasionally selectable in accordance with the conditions such as the water pressure and water dosage or the like.

In general, the pore diameter (by Tyler standard) of the porous element is in the range of 20 to 250 meshes (0.833 mm to 0.061 mm). The porous element having the pore diameter more than 120 meshes is selected so as to form the microscopic bubbles less than 10 μm in diameter. As the pore diameter is larger (as the value of mm is smaller), highly-concentrated dissolved hydrogen content can be acquired, thereby increasing a pressure drop and decreasing the production efficiency. Accordingly, the pore diameter of the porous element is occasionally selectable, depending on the required dissolved hydrogen content and the water dosage.

More than one tubular structures are connected and used in the manufacturing equipment of the hydrogen-added water according to the present invention. More than 1.3 ppm of the dissolved hydrogen content with water dosage of more than 15 L/min. can be ensured by connecting and using more than one tubular structures.

Due to the above construction, the first embodiment of the present invention is a method for manufacturing a hydrogen-added water;

said method, wherein a diffusion chamber having double tubes is provided and a plurality of tubular structures, in which porous element having predetermined pore diameters in the diffusion chamber is provided, are substantially linearly arranged in a longitudinal direction and a raw water and the hydrogen are supplied with one of the tubular structures, so as to form the mixture fluid of the raw water and the hydrogen by mixing the supplied raw water and hydrogen in the diffusion chamber, the mixture fluid is passed through the porous element and diffused therein, the mixture fluid of the raw water and hydrogen passed through the porous elements is supplied with the adjacent tubular structure under high pressure, so as to mix it with the hydrogen in the diffusion chamber of the adjacent tubular structure as well as to pass it through the porous element and diffuse therein, so that the hydrogen-added water containing a large amount of the microscopic bubbles of the hydrogen gas can be continuously produced.

The diameters of the microscopic bubbles may be in the range of 120 μm to 2 μm. The pore diameter of the porous element may be in the range of 120 μm to 2 μm. The porous element may be a sintered body of a metal or a ceramics.

The second embodiment of the present invention is a manufacturing equipment for a hydrogen-added water, comprising a tubular structure, both ends of which are formed in an open state, a raw water-supplying system that is formed on one end of the tubular structure and supplies the raw water under high pressure, a hydrogen supplying system that is watertightly connected to the tubular structure and supplies the hydrogen substantially at a right angle toward the raw water supplied from the raw water-supplying system, a diffusion chamber that is formed in a longitudinal direction of the tubular structure downstream of the hydrogen supplying system in the tubular structure so as to diffuse a mixture fluid of the raw water supplied from the raw water-supplying system to the tubular structure and the hydrogen supplied from the hydrogen supplying system to the tubular structure, a porous element having a predetermined pore diameter, which is filled with the diffusion chamber so as to pass through the mixture fluid of the supplied raw water and hydrogen, and an outlet that is formed on the other end of the tubular structure so as to discharge mixture fluid of the raw water and the hydrogen passed through the porous element, wherein a plurality of the tubular structures connects the adjacent raw water-supplying system to the outlet and is substantially linearly arranged in a longitudinal direction and the mixture fluid of the raw water and the hydrogen discharged from one of the tubular structure is supplied from the adjacent raw water-supplying system of the tubular system to the tubular structure under high pressure and mixed with the hydrogen in the adjacent diffusion chamber of the tubular structure so as to pass through the porous element and diffuse, so that the hydrogen-added water containing a large amount of microscopic bubble of the hydrogen gas is continuously produced.

The diameters of the microscopic bubbles may be in the range of 120 μm to 2 μm. The pore diameters of the porous element may be in the range of 120 μm to 2 μm. The porous element may be a sintered body of a metal or ceramics. A supply pressure of the raw water may be 0.1 to 0.5 MPa. A supply of the raw water may be 8 to 20 L/min. A supply pressure of the hydrogen may be 0.2 to 0.8 MPa. A supply of the hydrogen may be 0.1 to 1 L/min.

According to the first embodiment of the present invention, the hydrogen-added water containing a large amount of hydrogen gas as the mixture bubbles is commercially available for drinking with packaging in the predetermined container. Because the hydrogen-added water contains a large amount of hydrogen gas as the mixture bubbles, it has high absorption efficiency into the living organism and is superior in the homogeneity and the homogeneity, thereby applying it to the depuration of the water as well as the diagnosis and therapy of cancer or the like by using the performance of improving the biological activity of the living organism. The hydrogen-added water containing the hydrogen gas as the mixture bubbles can be continuously produced by maintaining the oxidation-reduction potential in the prescribed range and by keeping the pH in neutral.

Also, the diameters of the microscopic bubbles in the hydrogen gas are in the range of 120 μm to 2 μm, thereby increasing the application potentiality of the produced hydrogen-added water to the depuration of the water as well as to the diagnosis and therapy of cancer or the like.

the diameters of the microscopic bubbles in the porous element are in the range of 120 μm to 2 μm, thereby easily adjusting the diameters of the microscopic bubbles in the range of 120 μm to 2 μm.

The porous element is made up of the sintered body such as the metal or the ceramics, thereby improving the durability and the reliability of the pores in the porous element.

According to the second embodiment of the present invention, the hydrogen-added water containing a large amount of hydrogen gas as the mixture bubbles is commercially available for drinking with packaging in the predetermined container. Because the hydrogen-added water contains a large amount of hydrogen gas as the mixture bubbles, it has high absorption efficiency into the living organism and is superior in the homogeneity and the homogeneity, thereby applying it to the depuration of the water as well as to the diagnosis and therapy of cancer or the like by using the performance of improving the biological activity of the living organism. The hydrogen-added water containing the hydrogen gas as the mixture bubbles can be continuously produced by maintaining the oxidation-reduction potential in the prescribed range and by keeping the pH in neutral. The miniaturization and simplification of the equipment can expand its applications.

Also, the diameters of the microscopic bubbles in the hydrogen gas are in the range of 120 μm to 2 μm, thereby increasing the application potentiality of the produced hydrogen-added water to the depuration of the water as well as to the diagnosis and therapy of cancer or the like.

the diameters of the microscopic bubbles in the porous element are in the range of 120 μm to 2 μm, thereby easily adjusting the diameters of the microscopic bubbles in the range of 120 μm to 2 μm.

The porous element is made up of the sintered body such as the metal or the ceramics, thereby improving the durability and the reliability of the pores in the porous element.

Because the supply pressure of the raw water is 0.1 to 0.5 MPa or the supply of the raw water is 8 to 20 L/min., ordinary tap water (indifferent water) can be used as the raw water, thereby extending the range of use.

The supply pressure of the raw water is 0.2 to 0.8 MPa or the supply of the raw water is 0.1 to 1 L/min., thereby easily containing 0.5 to 1.6 ppm of the hydrogen.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a cross-sectional view of the produced hydrogen-added water manufacturing equipment according to one embodiment of the present invention.

FIG. 2 is a cross-sectional view of the produced hydrogen-added water manufacturing equipment according to another embodiment of the present invention.

FIG. 3 is a cross-sectional view of the produced hydrogen-added water manufacturing equipment according to yet another embodiment of the present invention.

1 . . . hydrogen-added water, 2 . . . raw water-supplying port, 3 . . . hydrogen supplying port, 4 . . . nozzle, 5 diffusion chamber, 6 porous element, 7 . . . outlet

DETAILED DESCRIPTION OF THE INVENTION

Hereinafter, preferred embodiments of the present invention will be described.

Example 1

FIG. 1 is a cross-sectional view of the produced hydrogen-added water manufacturing equipment according to one embodiment of the present invention. Referred to FIG. 1, a hydrogen-added water manufacturing equipment 1 is composed of the tubular structure made from the stainless steel and a raw water-supplying port 2 is provided as a raw water-supplying system. The raw water-supplying port 2 is watertightly connected to a tap water-supplying port, a pump, a piping or the like (not shown). A hydrogen supplying port 3 is provided as a hydrogen supplying system in the hydrogen-added water manufacturing equipment 1. The hydrogen supplying port 3 is watertightly connected to a hydrogen cylinder, a gas pressure controlling device, the piping or the like (not shown). The hydrogen supplying port 3 is configured so that the hydrogen is injected substantially at a right angle toward the raw water. A tapered nozzle 4 is connected to the apex of the raw water-supplying port 2, so that the raw water is injected under high pressure.

A diffusion chamber 5 having a double-tube construction is formed in the hydrogen-added water manufacturing equipment 1. The diffusion chamber 5 is formed so as to taper from both ends toward the center, i.e. to narrow down, so that the negative pressure is generated at the narrowed portion. An outlet 7 so as to discharge the produced hydrogen-added water is formed on the apex of the downstream portion of the diffusion chamber 5.

A porous element 6 is filled in the tapered portion of the diffusion chamber 5. For example, as mentioned below, a sintered body of the stainless steel having the thickness of 10 mm and the pore diameter of 200 meshes (0.074 mm) is used as the porous element 6.

Next, a method for manufacturing the hydrogen-added water using the hydrogen-added water manufacturing equipment 1 will be described.

In the present embodiment, first, the tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degrees) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.2 MPa, in a water dosage of 15 L/min. The hydrogen gas was injected from the hydrogen supplying port 3 at the gas pressure of 0.25 MPa using the gas pressure controlling device, in the water usage of 0.5 L/min, so as to form the mixture fluid of the raw water and the hydrogen.

The mixture fluid was diffused in the diffusion chamber 5 through the porous element 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 200 meshes (0.074 mm), in the water usage of 10 L/min., at the water temperature of 13.3 degrees, in the dissolved hydrogen content of 1.31 ppm, at the oxidation-reduction potential=−615 mV and pH=7.35, can be continuously obtained from the outlet 7.

Example 2

In the second embodiment, the same equipment as the hydrogen-added water manufacturing equipment 1 used in the first embodiment was used, except for changing the thickness of the porous element 6 to 5 mm.

The tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degrees) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.2 MPa, in a water dosage of 15 L/min. The hydrogen gas was injected from the hydrogen supplying port 3 at the gas pressure of 0.25 MPa 2 MPa using the gas pressure controlling device, in the water usage of 0.5 L/min, so as to form the mixture fluid of the raw water and the hydrogen. The mixture fluid was diffused in the diffusion chamber 5 through the porous element 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 200 meshes (0.074 mm), in the water usage of 12 L/min., at the water temperature of 13.3 degrees, in the dissolved hydrogen content of 0.9 ppm, at the oxidation-reduction potential=−600 mV and pH=7.30 can be continuously obtained from the outlet 7.

Example 3

In the third embodiment, the same equipment as the hydrogen added-water manufacturing equipment 1 used in the first embodiment was used, except for changing the thickness of the porous element 6 to 10 mm and changing the pore diameter to 60 meshes (0.246 mm).

The tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degrees) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.2 MPa, in a water dosage of 15 L/min. The hydrogen gas was injected from the hydrogen supplying port 3 at the gas pressure of 0.25 MPa using the gas pressure controlling device, in the water usage of 0.5 L/min so as to form the mixture fluid of the raw water and the hydrogen. The mixture fluid was diffused in the diffusion chamber 5 through the porous element 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 60 meshes (0.246 mm), in the water usage of 12 L/min., at the water temperature of 13.3 degrees, in the dissolved hydrogen content of 0.92 ppm, at the oxidation-reduction potential=−600 mV and pH=7.31 can be continuously obtained from the outlet 7.

Example 4

In the fourth embodiment, the same equipment as the hydrogen-added water manufacturing equipment 1 used in the first embodiment was used, except for changing the thickness of the porous element 6 to 5 mm and changing the pore diameter to 60 meshes (0.246 mm).

The tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degrees) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.2 MPa, in a water dosage of 15 L/min. The hydrogen gas was injected from the hydrogen supplying port 3 at the gas pressure of 0.25 MPa using the gas pressure controlling device, in the water usage of 0.5 L/min so as to form the mixture fluid of the raw water and the hydrogen. The mixture fluid was diffused in the diffusion chamber 5 through the porous element 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 60 meshes (0.246 mm), in the water usage of 14 L/min., at the water temperature of 13.3 degrees, in the dissolved hydrogen content of 0.75 ppm, at the oxidation-reduction potential=−600 mV and pH=7.28 can be continuously obtained from the outlet 7.

Example 5

FIG. 2 is a cross-sectional view of the equipment according to the fifth embodiment of the present invention. The equipment used in the fifth embodiment includes the structure to which two of the hydrogen-added water manufacturing equipment 1 of the first embodiment, equipped with the porous element 6 having the thickness of 10 mm and the pore diameter of 200 meshes (0.074 mm), are connected.

More specifically, two of the tubular structures, of which connect the adjacent hydrogen supplying port 3 and outlet 7, is substantially linearly arranged in a longitudinal direction. The mixture fluid of the raw water and the hydrogen discharged from one outlet 7 is supplied from the adjacent hydrogen supplying port 3 to the tubular structure under high pressure, and is continuously mixed with the hydrogen in the adjacent diffusion chamber 5 of the tubular structure.

The tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degrees) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.2 MPa, in a water dosage of 20 L/min. The hydrogen gas was injected from two of the hydrogen supplying ports 3, 3 at the gas pressure of 0.25 MPa using the gas pressure controlling device, in the water usage of 0.5 L/min. so as to form the mixture fluid of the raw water and the hydrogen. The mixture fluid was diffused in two of the diffusion chambers 5, 5 through two of the porous elements 6, 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 200 meshes (0.074 mm), in the water usage of 15 L/min., at the water temperature of 13.3 degrees, in the dissolved hydrogen content of 1.7 ppm, at the oxidation-reduction potential=−625 mV and pH=7.31 can be continuously obtained from the outlet 7.

Example 6

FIG. 3 is a cross-sectional view of the equipment according to the sixth embodiment. The equipment used in the sixth embodiment includes the structure to which three of the hydrogen-added water manufacturing equipment 1 of the first embodiment, equipped with the porous element 6 having the thickness of 10 mm and the pore diameter of 60 meshes (0.246 mm).

The tap water (the oxidation-reduction potential=357 mV, pH=7.25, the dissolved hydrogen content=3 ppb and a water temperature=13.2 degree s) in the waterworks department of Fukuyama City, Hiroshima Prefecture was injected from the raw water-supplying port 2 at a water pressure of 0.25 MPa, in a water dosage of 0.5 L/min. The hydrogen gas was injected from three of the hydrogen supplying ports 3, 3 and 3 at the gas pressure of 0.25 MPa, in the water usage of 0.5 L/min so as to form the mixture fluid of the raw water and the hydrogen. The mixture fluid was diffused in three of the diffusion chambers 5, 5 and 5 through three of the porous elements 6, 6 and 6. Consequently, the hydrogen-added water, containing a large amount of the microscopic bubble involving 60 meshes (0.246 mm), in the water usage of 15 L/min., in the dissolved hydrogen content of 1.52 ppm, at the oxidation-reduction potential=−623 mV and pH=7.31 can be continuously obtained from the outlet 7.

INDUSTRIAL APPLICABILITY

The present invention can apply the hydrogen-added water containing a large amount of the microscopic bubble of the hydrogen gas, which produced by the method for manufacturing the hydrogen-added water and the manufacturing equipment for the same, not only to the drinking water but also to the depuration of the water quality and the diagnosis/therapy or the like. 

1. A method for manufacturing a hydrogen-added water rich in microscopic bubbles of hydrogen gas comprising the steps of supplying raw water and hydrogen to one of tubular structures, wherein tubular structures are substantially linearly arranged in a longitudinal direction, wherein the tubular structure is a diffusion chamber of double tubes structure and a porous element having predetermined pore diameters in the diffusion chamber; mixing the supplied raw water and hydrogen in the diffusion chamber to make the mixture fluid of the raw water and the hydrogen; passing the mixture fluid through the porous element and diffusing the mixture fluid; providing the mixture fluid of the raw water and hydrogen passed through the porous elements to an adjacent tubular structure under high pressure; and passing the mixture fluid through the porous element and diffusing the mixture fluid after mixing the mixture fluid with hydrogen in the diffusion chamber of the adjacent tubular structure.
 2. The method for manufacturing the hydrogen-added water as set forth in claim 1, wherein the diameters of the microscopic bubbles are in the range of 120 μm to 2 μm.
 3. The method for manufacturing the hydrogen-added water as set forth in claim 1, wherein the pore diameters of the porous element are in the range of 120 μm to 2 μm.
 4. The method for manufacturing the hydrogen-added water as set forth in claim 1, wherein the porous element is a sintered body of a metal or ceramics.
 5. A manufacturing equipment for a hydrogen-added water, comprising; a tubular structure, both ends of which are formed in an open state, a raw water-supplying system that is formed on one end of the tubular structure and supplies the raw water under high pressure, a hydrogen supplying system that is watertightly connected to the tubular structure and supplies the hydrogen substantially at a right angle toward the raw water supplied from the raw water-supplying system, a diffusion chamber that is formed in a longitudinal direction of the tubular structure downstream of the hydrogen supplying system in the tubular structure so as to diffuse a mixture fluid of the raw water supplied from the raw water-supplying system to the tubular structure and the hydrogen supplied from the hydrogen supplying system to the tubular structure, a porous element having a predetermined pore diameter, which is filled with the diffusion chamber so as to pass through the mixture fluid of the supplied raw water and hydrogen, an outlet that is formed on the other end of the tubular structure so as to discharge mixture fluid of the raw water and the hydrogen passed through the porous element, wherein a plurality of the tubular structures connects the adjacent raw water-supplying system to the outlet and is substantially linearly arranged in a longitudinal direction and the mixture fluid of the raw water and the hydrogen discharged from one of the tubular structure is supplied from the adjacent raw water-supplying system of the tubular system to the tubular structure under high pressure and mixed with the hydrogen in the adjacent diffusion chamber of the tubular structure so as to pass through the porous element and diffuse, so that the hydrogen-added water containing a large amount of microscopic bubble of the hydrogen gas is continuously produced.
 6. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein the diameters of the microscopic bubbles is in the range of 120 μm to 2 μm.
 7. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein the pore diameters of the porous element are in the range of 120 μm to 2 μm.
 8. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein the porous element is a sintered body of a metal or ceramics.
 9. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein a supply pressure of the raw water is 0.1 to 0.5 MPa.
 10. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein a supply of the raw water is 8 to 20 L/min.
 11. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein a supply pressure of the hydrogen is 0.2 to 0.8 MPa.
 12. The manufacturing equipment for a hydrogen-added water as set forth in claim 5, wherein a supply of the hydrogen is 0.1 to 1 L/min. 